US10436096B2 - Heat exchanger and method for controlling heat exchanger - Google Patents
Heat exchanger and method for controlling heat exchanger Download PDFInfo
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- US10436096B2 US10436096B2 US15/548,619 US201515548619A US10436096B2 US 10436096 B2 US10436096 B2 US 10436096B2 US 201515548619 A US201515548619 A US 201515548619A US 10436096 B2 US10436096 B2 US 10436096B2
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- heat
- flue gas
- heat exchange
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- 238000000034 method Methods 0.000 title claims description 26
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 175
- 239000003546 flue gas Substances 0.000 claims abstract description 175
- 238000011084 recovery Methods 0.000 claims abstract description 88
- 238000010438 heat treatment Methods 0.000 claims abstract description 67
- 239000007789 gas Substances 0.000 claims description 20
- 238000002485 combustion reaction Methods 0.000 claims description 12
- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical compound [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 claims description 5
- 239000000428 dust Substances 0.000 description 24
- 238000005260 corrosion Methods 0.000 description 20
- 230000007797 corrosion Effects 0.000 description 20
- 238000006477 desulfuration reaction Methods 0.000 description 16
- 230000023556 desulfurization Effects 0.000 description 16
- 238000005259 measurement Methods 0.000 description 12
- 238000003915 air pollution Methods 0.000 description 11
- 239000012716 precipitator Substances 0.000 description 9
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000003595 mist Substances 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 3
- 230000002745 absorbent Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910052815 sulfur oxide Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000003303 reheating Methods 0.000 description 2
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N5/00—Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N9/00—Electrical control of exhaust gas treating apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/08—Arrangements of devices for treating smoke or fumes of heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2215/00—Preventing emissions
- F23J2215/20—Sulfur; Compounds thereof
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
- F23J2900/15081—Reheating of flue gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
- F28F2250/06—Derivation channels, e.g. bypass
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
-
- Y02E20/348—
-
- Y02E20/363—
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
-
- Y02T10/16—
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/40—Engine management systems
-
- Y02T10/47—
Definitions
- the present invention relates to a heat exchanger and a method for controlling the heat exchanger, for example, a heat exchanger that includes a preheating unit for preheating flue gas introduced into a reheater and a method for controlling the heat exchanger.
- An air pollution control device is used in thermal power plants and chemical plants.
- a denitration device an air preheating unit air heater, a heat recovery unit of a reheating heat exchanger (gas-gas heater), a dry electronic precipitator, a wet desulfurization device, a reheater of the reheating heat exchanger, and a stack are sequentially provided from the upstream side toward the downstream side of a flue gas flow path.
- a gas-gas heater including a preheating unit that is provided on a flue gas introduction portion of a reheater and that preheats flue gas introduced into the reheater body has been developed as the heat exchanger used in the air pollution control device such as the above (for example, see Patent Literature 1).
- wet flue gas that has passed through the wet desulfurization device is preheated and dried in the preheating unit supplied with a heat medium having been heated by the heat recovery unit and the heating unit. Because the flue gas is dried, it is possible to reduce dust in the flue gas from adhering to the inside of the reheater body and reduce corrosion inside of the reheater body resulting from wet components in the flue gas.
- Patent Literature 1 Japanese Laid-open Patent Publication No. 2011-094901
- the heat exchanger is controlled so that the temperature of the flue gas at the flue gas outlet portion of the heat recovery unit and the temperature of the heat medium at the heat medium outlet portion of the reheater will fall within respective predetermined ranges.
- the gas temperature and the gas flow of the flue gas introduced into the air pollution control device may be reduced by the variation in the power generation load corresponding to the change in the operating conditions.
- the temperature of the heat medium at the heat medium inlet portion of the reheater may be reduced by the change in the heat quantity of the flue gas recovered by the heat recovery unit.
- the present invention has been made in view of the above circumstances, and an object of the present invention is to provide a heat exchanger and a method for controlling the heat exchanger capable of reducing dust in the flue gas from adhering to the inside of the reheater and reducing corrosion of the heat transfer tube, even if the operating conditions have changed.
- a heat exchanger comprising: a heat recovery unit that causes a heat medium to recover heat from flue gas from a combustion engine through first heat exchange by bringing the flue gas into contact with a heat transfer tube in which the heat medium flows; a reheater that includes a preheating unit configured to preheat the flue gas after the first heat exchange through second heat exchange by bringing the flue gas after the first heat exchange into contact with the heat transfer tube in which the heat medium after the first heat exchange flows, and a heating unit configured to heat the flue gas after the second heat exchange through third heat exchange by bringing the flue gas after the second heat exchange into contact with the heat medium after the second heat exchange; a circulation line that circulates the heat medium between the heat recovery unit and the reheater; and a control unit that calculates a recovered heat quantity to be recovered by the heat recovery unit from the flue gas through the first heat exchange, and that controls temperature of the heat medium after the first heat exchange within a predetermined range based on the calculated recovered heat quantity.
- the temperature of the heat medium to be supplied to the preheating unit of the reheater is controlled on the basis of the recovered heat quantity that is recovered by the heat recovery unit from the flue gas introduced into the heat recovery unit. Consequently, it is possible to set the temperature of the heat medium to be supplied to the preheating unit within a predetermined range without delay, according to the change in the recovered heat quantity that is recovered by the heat recovery unit from the flue gas. In this manner, even if the operating conditions of a boiler and the like have changed, it is possible to implement the heat exchanger and the method for controlling the heat exchanger capable of reducing dust in the flue gas from adhering to the inside of the reheater, and reduce corrosion of the heat transfer tube of the preheating unit.
- the control unit calculates the recovered heat quantity based on at least one type selected from the group consisting of gas temperature of the flue gas introduced into the heat exchanger, a gas flow of the flue gas, and operation load of the combustion engine.
- the accuracy of the recovered heat quantity calculated by the control unit will be improved. Consequently, it is possible to further reduce dust in the flue gas from adhering to the inside of the reheater and reduce corrosion of the heat transfer tube of the preheating unit.
- the control unit heats the heat medium after the first heat exchange, when the recovered heat quantity is less than a predetermined value.
- the heat medium can be heated according to the recovered heat quantity. Consequently, it is possible to reduce dust in the flue gas from adhering to the inside of the reheater and reduce corrosion of the heat transfer tube of the preheating unit.
- control unit supplies steam to the heat medium after the first heat exchange from a steam supply unit, and sets the temperature of the heat medium after the first heat exchange within the predetermined range.
- the circulation line includes a bypass line that bypasses the heat recovery unit, and the control unit sets the temperature of the heat medium within the predetermined range, by circulating the heat medium between the heat recovery unit and the reheater via the bypass line, when the recovered heat quantity exceeds the predetermined value.
- a plurality of heat transfer tubes of the heating unit are arranged in a tetragonal lattice pattern relative to a flowing direction of the flue gas.
- a method for controlling a heat exchanger that includes a heat recovery unit that causes a heat medium to recover heat from flue gas from a combustion engine through first heat exchange by bringing the flue gas into contact with a heat transfer tube in which the heat medium flows; and a reheater that includes a preheating unit configured to preheat the flue gas after the first heat exchange using heat of the heat medium after the first heat exchange through second heat exchange by bringing the flue gas after the first heat exchange into contact with the heat transfer tube in which the heat medium after the first heat exchange flows, and a heating unit configured to heat the flue gas after the second heat exchange through third heat exchange by bringing the flue gas after the second heat exchange into contact with the heat medium after the second heat exchange, the method for controlling the heat exchanger, comprising: a step of calculating a recovered heat quantity to be recovered by the heat recovery unit from the flue gas through the first heat exchange; and a step of controlling temperature of the heat medium within a predetermined range by heating the heat medium after the first heat exchange, when the calculated recovered heat
- the temperature of the heat medium to be supplied to the preheating unit of the reheater is controlled on the basis of the recovered heat quantity that is recovered by the heat recovery unit from the flue gas introduced into the heat recovery unit. Consequently, it is possible to set the temperature of the heat medium to be supplied to the preheating unit within a predetermined range without delay, according to the change in the recovered heat quantity that is recovered by the heat recovery unit from the flue gas. In this manner, even if the operating conditions of the boiler and the like have changed, it is possible to implement the heat exchanger and the method for controlling the heat exchanger capable of reducing dust in the flue gas from adhering to the inside of the reheater, and reduce corrosion of the heat transfer tube of the preheating unit. With this configuration, even if the heat quantity recovered by the heat recovery unit is too large, it is possible to reduce the heat quantity recovered by the heat recovery unit, and set the temperature of the heat medium within a predetermined range.
- the method for controlling a heat exchanger it is preferable that the method further comprising a step of controlling the temperature of the heat medium within the predetermined range by making the heat medium flow in a bypass line that bypasses the heat recovery unit, when the calculated recovered heat quantity exceeds the predetermined value.
- the present invention even if the operating conditions have changed, it is possible to implement the heat exchanger and the method for controlling the heat exchanger capable of reducing dust in the flue gas from adhering to the inside of the reheater and reduce corrosion of the heat transfer tube.
- FIG. 1 is schematic diagram of an air pollution control system according to a first embodiment of the present invention.
- FIG. 2 is a schematic view of a heat exchanger according to the first embodiment of the present invention.
- FIG. 3 is a flow chart of a method for controlling the heat exchanger according to the first embodiment of the present invention.
- FIG. 4 is a schematic view of a heat exchanger according to a second embodiment of the present invention.
- FIG. 5 is a flow chart of a method for controlling the heat exchanger according to the embodiment of the present invention.
- FIG. 6A is a diagram illustrating an example of a configuration of a reheater according to the embodiment of the present invention.
- FIG. 6B is a diagram illustrating another example of the configuration of the reheater according to the embodiment of the present invention.
- FIG. 1 is a schematic diagram of an air pollution control system 10 according to a first embodiment of the present invention.
- the air pollution control system 10 according to the present embodiment is an air pollution control system that treats flue gas discharged from a thermal power plant, a chemical plant, or the like, and that removes nitrogen oxides (NOx), dust, and sulfur oxides (SOx) included in the flue gas to discharge.
- NOx nitrogen oxides
- SOx sulfur oxides
- the air pollution control system 10 includes a boiler 11 installed in a thermal power plant, a chemical plant, and the like, a denitration device 12 provided at a subsequent stage of the boiler 11 , an air heater (AH) 13 provided at a subsequent stage of the denitration device 12 , and an electronic precipitator 14 provided at a subsequent stage of the air heater 13 .
- the air pollution control system 10 also includes an air blower 15 provided at a subsequent stage of the electronic precipitator 14 , a desulfurization device 16 provided at a subsequent stage of the air blower 15 , and a stack 17 provided at a subsequent stage of the desulfurization device 16 .
- a heat recovery unit 21 of a heat exchanger 20 according to the present embodiment is disposed between the air heater 13 and the electronic precipitator 14 .
- a reheater 22 of the heat exchanger (gas-gas heater) 20 according to the present embodiment is disposed between the desulfurization device 16 and the stack 17 .
- a fin tube 21 a as a heat transfer tube in which a heat medium flows is provided inside the heat recovery unit 21 .
- the reheater 22 includes a preheating unit 221 that preheats the flue gas introduced into the reheater 22 , a low-temperature heating unit 222 that heats the flue gas preheated by the preheating unit 221 , and a high-temperature heating unit 223 that further heats the flue gas heated by the low-temperature heating unit 222 .
- a tube 221 a is disposed inside the preheating unit 221 as a heat transfer bare tube.
- a fin tube 222 a is disposed inside the low-temperature heating unit 222 as a heat transfer tube.
- a fin tube 223 a is disposed inside the high-temperature heating unit 223 as a heat transfer tube.
- a circulation line L that circulates a heat medium M between the heat recovery unit 21 and the reheater 22 is provided between the heat recovery unit 21 and the reheater 22 .
- a liquid feeding pump P that circulates the heat medium M in the circulation line L between the heat recovery unit 21 and the reheater 22 is provided on the circulation line L. Heat exchange is performed between the heat recovery unit 21 and the reheater 22 , using the heat medium M that flows in the circulation line L by the liquid feeding pipe P.
- Flue gas G 0 discharged from the boiler 11 is introduced into the denitration device 12 filled with a catalyst.
- the flue gas G 0 introduced into the denitration device 12 is made harmless by reducing the nitrogen oxides included in the flue gas G 0 to water and nitrogen, with ammonia (NH 3 ) injected into the denitration device 12 as a reducing agent.
- Flue gas G 1 discharged from the denitration device 12 is introduced into the air heater (AH) 13 .
- the temperature of the flue gas G 1 introduced into the air heater 13 is cooled to equal to or more than 130 degrees Celsius and equal to or less than 150 degrees Celsius, by heat exchange with air.
- Flue gas G 2 discharged from the air heater 13 is introduced into the heat recovery unit 21 of the heat exchanger (gas-gas heater) 20 according to the present embodiment.
- the heat of the flue gas G 2 introduced into the heat recovery unit 21 is recovered and cooled by heat exchange with a heat medium (such as water), when the flue gas G 2 is brought into contact with the fin tube 21 a in which the heat medium M flows.
- a heat medium such as water
- the temperature of flue gas G 3 after the heat exchange in the heat recovery unit 21 is equal to or more than 85 degrees Celsius and equal to or less than 110 degrees Celsius.
- the flue gas G 3 discharged from the heat recovery unit 21 is introduced into the electronic precipitator (EP) 14 to remove dust.
- dust such as fly ash in the flue gas G 3 that is cooled by heat exchange in the heat recovery unit 21 is removed. Consequently, it is possible to improve the dust collection efficiency of the electronic precipitator 14 .
- the air blower 15 driven by a motor boosts the pressure of flue gas G 4 discharged from the electronic precipitator 14 . It is to be understood that the air blower 15 is not necessarily provided. The air blower 15 may also be provided at a subsequent stage of the reheater 22 of the heat exchanger 20 .
- Flue gas G 5 the pressure of which is boosted by the air blower 15 is introduced into the desulfurization device 16 .
- sulfur oxides in the flue gas G 5 are absorbed and removed by absorbent in which slurry limestone is dissolved, and gypsum (not illustrated) is generated as a by-product.
- flue gas G 6 discharged from the desulfurization device 16 absorbs water in the absorbent and becomes wet. The temperature of the flue gas G 6 is reduced to, for example, about 50 degrees Celsius.
- the flue gas G 6 discharged from the desulfurization device 16 is introduced into the heat recovery unit 21 of the heat exchanger (gas-gas heater) 20 according to the present embodiment.
- the flue gas G 6 introduced into the heat recovery unit 21 is sequentially brought into contact with the tube 221 a , the fin tube 222 a , and the fin tube 223 a in the preheating unit 221 , the low-temperature heating unit 222 , and the high-temperature heating unit 223 , and is heated by heat exchange with the heat medium.
- the preheating unit 221 heats the wet flue gas G 6 to the temperature exceeding 50 degrees Celsius in advance. Thus, the humidity of the wet flue gas G 6 is reduced.
- FIG. 2 is a schematic view of the heat exchanger 20 according to the present embodiment.
- the heat exchanger 20 includes the heat recovery unit 21 , the reheater 22 , and a steam supply unit 23 .
- the heat recovery unit 21 heats the heat medium M by causing the heat medium M to recover the heat from the flue gas G 2 that is introduced from the air heater 13 , and discharges the cooled flue gas G 3 after the heat is recovered, to the electronic precipitator 14 .
- the reheater 22 heats the wet flue gas G 6 introduced from the desulfurization device 16 with the heat medium M, and discharges the heated flue gas G 7 to the stack 17 .
- the steam supply unit 23 supplies steam S to the heat medium M in the circulation line L that supplies the heat medium M from the heat recovery unit 21 toward the reheater 22 .
- the heat medium M that is heated by the heat recovery unit 21 is transmitted to the reheater 22 by the liquid feeding pump P through the circulation line L.
- the heat medium M that is cooled by the reheater 22 is transmitted to the heat recovery unit 21 by the liquid feeding pump P through the circulation line L.
- the heat medium M is supplied to the circulation line L that supplies the heat medium M from the reheater 22 toward the heat recovery unit 21 , from a heat medium tank 24 as required.
- the fin tube 21 a is disposed inside the heat recovery unit 21 .
- the fin tube 21 a is a heat transfer tube obtained by providing a plurality of fins that are heat sinks on a tube-shaped member.
- the circulation line L for circulating the heat medium M between the heat recovery unit 21 and the reheater 22 is connected to the fin tube 21 a .
- the heat exchanger 20 heats the heat medium M by causing the heat medium M to recover the heat from the flue gas G 2 by first heat exchange in which the flue gas G 2 introduced into the heat recovery unit 21 from the air heater 13 is brought into contact with the fin tube 21 a .
- the heated heat medium M is transmitted toward the reheater 22 by the liquid feeding pump P provided on the circulation line L.
- the reheater 22 includes the preheating unit 221 , the low-temperature heating unit 222 , and the high-temperature heating unit 223 .
- the preheating unit 221 includes the tube 221 a as the heat transfer bare tube that is a tube-shaped member.
- the low-temperature heating unit 222 includes the fin tube 222 a as the heat transfer tube obtained by providing the fins that are heat sinks on a tube-shaped member.
- the high-temperature heating unit 223 includes the fin tube 223 a as the heat transfer tube obtained by providing the fins that are heat sinks on a tube-shaped member.
- One end of the tube 221 a is connected to the circulation line L, and the other end of the tube 221 a is connected to an end of the fin tube 223 a via the circulation line L.
- the other end of the fin tube 223 a is connected to one end of the fin tube 222 a via the circulation line L.
- the other end of the fin tube 222 a is connected to the circulation line L.
- the heat medium M after the first heat exchange that is supplied from the heat recovery unit 21 is sequentially transmitted through the preheating unit 221 , the high-temperature heating unit 223 , and the low-temperature heating unit 222 , in the order of the preheating unit 221 , the high-temperature heating unit 223 , and the low-temperature heating unit 222 .
- the heat medium M supplied to the low-temperature heating unit 222 is transmitted to the heat recovery unit 21 through the circulation line L.
- the preheating unit 221 heats the flue gas G 6 and reduces the humidity of the wet flue gas G 6 , by second heat exchange in which the wet flue gas G 6 introduced to the reheater 22 from the desulfurization device 16 is brought into contact with the heated heat medium M after the first heat exchange that is supplied from the heat recovery unit 21 .
- the preheating unit 221 also cools the heat medium M.
- the preheating unit 221 further supplies the flue gas G 6 after the second heat exchange and the humidity of which is reduced, to the low-temperature heating unit 222 and the high-temperature heating unit 223 .
- the preheating unit 221 also supplies the cooled heat medium M after the second heat exchange to the high-temperature heating unit 223 .
- the low-temperature heating unit 222 further heats the flue gas G 6 by third heat exchange in which the flue gas G 6 supplied from the preheating unit 221 is brought into contact with the heat medium M supplied from the high-temperature heating unit 223 .
- the low-temperature heating unit 222 also cools the heat medium M.
- the wet flue gas G 6 is heated by the preheating unit 221 and is turned into the flue gas G 6 the humidity of which is reduced. Consequently, it is possible to prevent dust accompanying the flue gas G 6 from adhering to the tube 221 a of the preheating unit 221 , and corrosion of the tube 221 a of the preheating unit 221 caused by the mist.
- the low-temperature heating unit 222 supplies the flue gas G 6 after the third heat exchange to the high-temperature heating unit 223 , and supplies the cooled heat medium M after the third heat exchange to the heat recovery unit 21 .
- the high-temperature heating unit 223 further heats the flue gas G 6 that is heated by fourth heat exchange in which the heated flue gas G 6 that is supplied from the low-temperature heating unit 222 is brought into contact with the heat medium M after the second heat exchange that is supplied from the preheating unit 221 .
- the high-temperature heating unit 223 also cools the heat medium M.
- the high-temperature heating unit 223 further supplies the flue gas G 7 after the third heat exchange to the stack 17 , and supplies the cooled heat medium M after the third heat exchange to the heat recovery unit 21 .
- the flue gas G 6 supplied from the preheating unit 221 is heated to sufficient temperature by the low-temperature heating unit 222 and the high-temperature heating unit 223 .
- the steam supply unit (heating unit) 23 supplies the steam S toward a heat exchanging unit 25 that is provided on the circulation line L for supplying the heat medium M toward the reheater 22 from the heat recovery unit 21 through a steam supply line L 1 .
- a flow control valve V 1 for controlling the flow of steam supplied to the heat exchanging unit 25 from the steam supply unit 23 is provided on the steam supply line L 1 .
- the heat exchanger 20 can sufficiently heat the wet flue gas G 6 in the preheating unit 221 of the reheater 22 . Consequently, it is possible to prevent dust in the flue gas G 6 from adhering to the tube 221 a of the preheating unit 221 , and corrosion of the tube 221 a caused by the mist.
- the heat exchanger 20 includes a flue gas measurement unit 31 and a control unit 32 .
- the flue gas measurement unit 31 is provided on an introduction portion of the flue gas G 2 that is introduced to the heat recovery unit 21 from the air heater 13 , in the heat recovery unit 21 .
- the control unit 32 controls the temperature of the heat medium M that flows in the circulation line L on the basis of a measurement value measured by the flue gas measurement unit 31 .
- the flue gas measurement unit 31 measures the gas flow of the flue gas G 2 introduced into the heat recovery unit 21 , the gas temperature of the flue gas G 2 , and the like and transmits the measurement values to the control unit 32 .
- the control unit 32 calculates the recovered heat quantity that is to be recovered to the heat medium M from the flue gas G 2 through the first heat exchange by the heat exchanger 20 , from introduction conditions of the flue gas G 2 to the heat recovery unit 21 .
- the introduction conditions are based on the various measurement values transmitted from the flue gas measurement unit 31 ; air volume supplied to an induced draft fan (IDF, not illustrated) that blows the flue gas G 0 after combustion from the boiler 11 , a boost up fan (BUF, not illustrated) provided on the desulfurization device 16 , as well as the boiler 11 ; combustion load of the boiler 11 ; and the like.
- the control unit 32 controls the flow of the steam S supplied to the heat medium M by the steam supply unit 23 and the flow control valve V 1 so that the temperature at an outlet portion of the circulation line L from the heat recovery unit 21 that is measured by a temperature measurement device T 1 will fall within a predetermined range, on the basis of the calculated recovered heat quantity.
- the heat exchanger 20 can speedily calculate the recovered heat quantity through the first heat exchange by the heat exchanger 20 , on the basis of the introduction conditions of the flue gas G 2 to the heat recovery unit 21 that is calculated by the control unit 32 . Because it is possible to set temperature T 2 at the outlet portion of the heat recovery unit 21 and temperature T 3 at the outlet portion of the reheater 22 within a predetermined range, even if the heat quantity recovered by the heat exchanger 20 is changed, it is possible to set the temperature of the heat medium M to be supplied to the preheating unit 221 of the reheater 22 within a predetermined range at an early stage. Consequently, it is possible to prevent dust from adhering to the tube 221 a of the preheating unit 221 , and corrosion of the tube 221 a of the preheating unit 221 at an early stage.
- FIG. 3 is a flow chart of the method for controlling the heat exchanger 20 according to the present embodiment.
- the method for controlling the heat exchanger 20 according to the present embodiment includes a first step of calculating the heat quantity recovered by the heat exchanger 20 , a second step of determining whether the calculated recovered heat quantity is less than a predetermined value, a third step of starting supplying the steam S to the heat medium M when the calculated recovered heat quantity is less than the predetermined value, and a fourth step (step ST 14 ) of stopping supplying the steam S to the heat medium M when the calculated recovered heat quantity exceeds the predetermined value.
- the control unit 32 calculates the recovered heat quantity that is to be recovered to the heat medium M from the flue gas G 2 through the first heat exchange by the heat exchanger 20 , from introduction conditions of the flue gas G 2 to the heat recovery unit 21 (step ST 11 ).
- the introduction conditions are based on the various measurement values transmitted from the flue gas measurement unit 31 ; air volume supplied to the induced draft fan (IDF, not illustrated) that blows the flue gas G 0 after combustion from the boiler 11 , the boost up fan (BUF, not illustrated) provided on the desulfurization device 16 , as well as the boiler 11 ; combustion load of the boiler 11 ; and the like.
- the control unit 32 determines whether the calculated recovered heat quantity is less than a predetermined value, by comparing the calculated recovered heat quantity with a predetermined threshold set in advance (step ST 12 ).
- the control unit 32 starts supplying the steam S from the steam supply unit 23 , and supplies the steam S to the heat medium M in the circulation line L by opening the flow control valve V 1 of the steam supply line L 1 (step ST 13 ). In this manner, it is possible to set the temperature of the heat medium M to be supplied to the preheating unit 221 of the reheater 22 within a predetermined range.
- the control unit 32 stops supplying the steam S from the steam supply unit 23 and stops supplying the steam S to the heat medium M in the circulation line L by closing the flow control valve V 1 of the steam supply line L 1 (step ST 14 ).
- the temperature of the heat medium M to be supplied to the preheating unit 221 of the reheater 22 is controlled on the basis of the recovered heat quantity that is recovered by the heat recovery unit 21 from the flue gas G 2 introduced into the heat recovery unit 21 . Consequently, it is possible to set the temperature of the heat medium M to be supplied to the preheating unit 221 within a predetermined range without delay, according to the change in the recovered heat quantity that is recovered by the heat recovery unit 21 from the flue gas G 2 .
- FIG. 4 is a schematic view of the heat exchanger 20 according to the second embodiment of the present invention.
- the heat exchanger 20 according to the present embodiment includes a bypass line L 2 provided between the circulation line L for supplying the heat medium M to the heat recovery unit 21 from the reheater 22 , and the circulation line L for supplying the heat medium M to the reheater 22 from the heat recovery unit 21 .
- a flow control valve V 2 for adjusting the flow of the heat medium M that flows in the bypass line L 2 is provided on the bypass line L 2 .
- the flow control valve V 2 is openable and closable by the control unit 32 .
- the control unit 32 adjusts the opening degree of the flow control valve V 2 according to the heat quantity recovered by the heat recovery unit 21 that is calculated by the control unit 32 .
- the control unit 32 adjusts the opening degree of the flow control valve V 2 according to the heat quantity recovered by the heat recovery unit 21 that is calculated by the control unit 32 .
- it is possible to control the flow of the heat medium M that flows in the bypass line L 2 . Consequently, even if the gas flow and the gas temperature of the flue gas G 2 to be supplied from the air heater 13 is high, it is possible to prevent excessive heat recovery by the heat recovery unit 21 and control the recovered heat quantity to be recovered to the heat medium M within a predetermined range.
- the other configurations are the same as those in the heat exchanger 20 according to the first embodiment described above, and the description thereof will be omitted.
- FIG. 5 is a flow chart of the method for controlling the heat exchanger 20 according to the present embodiment.
- the method for controlling the heat exchanger 20 according to the present embodiment includes a first step of calculating the heat quantity recovered by the heat exchanger 20 , a second step of determining whether the calculated recovered heat quantity is less than a predetermined range, a third step of starting supplying the steam S to the heat medium M when the calculated recovered heat quantity is less than the predetermined range, a fourth step of stopping supplying the steam S to the heat medium M when the calculated recovered heat quantity falls within the predetermined range, a fifth step of determining whether the calculated recovered heat quantity exceeds the predetermined range, a sixth step of opening the bypass line L 2 when the calculated recovered heat quantity exceeds the predetermined range, and a seventh step of closing the bypass line L 2 when the calculated recovered heat quantity falls within the predetermined range.
- the control unit 32 calculates the recovered heat quantity that is to be recovered to the heat medium M from the flue gas G 2 through the first heat exchange by the heat exchanger 20 , from introduction conditions of the flue gas G 2 to the heat recovery unit 21 (step ST 21 ).
- the introduction conditions are based on the various measurement values transmitted from the flue gas measurement unit 31 ; air volume supplied to the induced draft fan (IDF, not illustrated) that blows the flue gas G 0 after combustion from the boiler 11 , the boost up fan (BUF, not illustrated) provided on the desulfurization device 16 , as well as the boiler 11 ; combustion load of the boiler 11 ; and the like.
- the control unit 32 determines whether the calculated recovered heat quantity is less than the predetermined range by comparing the calculated recovered heat quantity with a predetermined threshold set in advance (step ST 22 ).
- the control unit 32 starts supplying the steam S from the steam supply unit 23 , and supplies the steam S to the heat medium M in the circulation line L by opening the flow control valve V 1 of the steam supply line L 1 (step ST 23 ). In this manner, it is possible to set the temperature of the heat medium M supplied to the preheating unit 221 of the reheater 22 within a predetermined range.
- the control unit 32 stops supplying the steam S from the steam supply unit 23 , and stops supplying the steam S to the heat medium M in the circulation line L by closing the flow control valve V 1 of the steam supply line L 1 (step ST 24 ).
- the control unit 32 determines whether the calculated recovered heat quantity exceeds the predetermined range by comparing the calculated recovered heat quantity with a predetermined threshold set in advance (step ST 25 ).
- the control unit 32 opens the flow control valve V 2 of the bypass line L 2 and circulates a part of the heat medium M to the reheater 22 through the bypass line L 2 without via the heat recovery unit 21 (step ST 26 ).
- the heat exchanger 20 can prevent the excessive recovery of heat quantity from the flue gas G 2 to be introduced into the heat recovery unit 21 . Consequently, it is possible to set the temperature of the heat medium M to be supplied to the preheating unit 221 of the reheater 22 within a predetermined range.
- the control unit 32 closes the flow control valve V 2 of the bypass line L 2 , and circulates the heat medium M between the reheater 22 and the heat recovery unit 21 without via the bypass line L 2 (step ST 27 ).
- the temperature of the heat medium M to be supplied to the preheating unit 221 of the reheater 22 and the supply of the heat medium M to the heat recovery unit 21 are controlled, on the basis of whether the recovered heat quantity that is recovered by the heat recovery unit 21 from the flue gas G 2 introduced into the heat recovery unit 21 falls within a predetermined range. Consequently, even if the recovered heat quantity that is recovered by the heat recovery unit 21 from the flue gas G 2 is equal to or more than the predetermined value, it is possible to set the temperature of the heat medium M to be supplied to the preheating unit 221 within a predetermined range without delay, according to the change in the recovered heat quantity that is recovered by the heat recovery unit 21 from the flue gas G 2 .
- the arrangement configuration of the tube 221 a of the preheating unit 221 , the fin tube 222 a of the low-temperature heating unit 222 , and the fin tube 223 a of the high-temperature heating unit 223 in the reheater 22 of the first embodiment and the second embodiment described above is not particularly limited as long as it is possible to heat the flue gas G 6 to be introduced into the reheater 22 to a predetermined temperature.
- FIG. 6A is a diagram illustrating an example of a configuration of the reheater 22 .
- FIG. 6A is a schematic view of a vertical section of a plurality of the tubes 221 a , the fin tubes 222 a , and the fin tubes 223 a of the preheating unit 221 , the low-temperature heating unit 222 , and the high-temperature heating unit 223 of the reheater 22 relative to the extending direction of the tubes 221 a , the fin tubes 222 a , and the fin tubes 223 a.
- the tubes 221 a , the fin tubes 222 a , and the fin tubes 223 a of the preheating unit 221 , the low-temperature heating unit 222 , and the high-temperature heating unit 223 may be arranged in a lattice pattern relative to the flowing direction of the flue gas G 6 and the flue gas G 7 in the sectional view, respectively.
- the contact area of the tubes 221 a , the fin tubes 222 a , and the fin tubes 223 a relative to the flue gas G 6 that is introduced into the reheater 22 is increased. Consequently, it is possible to efficiently heat the flue gas G 6 and discharge the flue gas G 6 as the flue gas G 7 .
- FIG. 6B is a diagram illustrating another example of the configuration of the reheater 22 . Similar to FIG. 6A , FIG. 6B is a schematic view of a vertical section of the tubes 221 a , the fin tubes 222 a , and the fin tubes 223 a of the preheating unit 221 , the low-temperature heating unit 222 , and the high-temperature heating unit 223 of the reheater 22 relative to the extending direction of the tubes 221 a , the fin tubes 222 a , and the fin tubes 223 a.
- the tubes 221 a and the fin tubes 223 a of the preheating unit 221 and the high-temperature heating unit 223 are arranged in a lattice pattern relative to the flowing direction of the flue gas G 6 and the flue gas G 7 in the sectional view, respectively.
- the fin tubes 222 a of the low-temperature heating unit 222 are arranged in a tetragonal lattice pattern relative to the flowing direction of the flue gas G 6 and the flue gas G 7 in the sectional view, respectively.
- the contact area of the tubes 221 a and the fin tubes 223 a relative to the flue gas G 6 introduced into the reheater 22 is increased, and a sufficient contact area can be obtained.
- the contact area between the flue gas G 6 and the fin tubes 222 a can be moderately reduced, thereby improving the flow velocity of the flue gas G 6 that passes through the low-temperature heating unit 222 .
- the gas flow velocity of the flue gas G 6 that flows through the high-temperature heating unit 223 is further improved. Consequently, it is possible to efficiently heat the flue gas G 6 and discharge the flue gas G 6 as the flue gas G 7 . As a result, it is also possible to further reduce dust from adhering to the fin tube 222 a of the low-temperature heating unit 222 and reduce corrosion of the fin tube 222 a of the low-temperature heating unit 222 caused by the mist.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Chimneys And Flues (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
-
- 10 air pollution control system
- 11 boiler
- 12 denitration device
- 13 air heater
- 14 electronic precipitator
- 15 air blower
- 16 desulfurization device
- 17 stack
- 20 heat exchanger
- 21 heat recovery unit
- 21 a fin tube
- 22 reheater
- 221 preheating unit
- 222 low-temperature heating unit
- 223 high-temperature heating unit
- 221 a tube
- 222 a, 223 a fin tube
- G0, G1, G2, G3, G4, G5, G6, G7 flue gas
- L circulation line
- L1 steam supply line
- M heat medium
- P liquid feeding pump
- S steam
- V1, V2 flow control valve
Claims (8)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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JP2015-021429 | 2015-02-05 | ||
JP2015021429A JP6632198B2 (en) | 2015-02-05 | 2015-02-05 | Heat exchanger and heat exchanger control method |
PCT/JP2015/081040 WO2016125353A1 (en) | 2015-02-05 | 2015-11-04 | Heat exchanger and method for controlling heat exchanger |
Publications (2)
Publication Number | Publication Date |
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US20180010504A1 US20180010504A1 (en) | 2018-01-11 |
US10436096B2 true US10436096B2 (en) | 2019-10-08 |
Family
ID=56563712
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Application Number | Title | Priority Date | Filing Date |
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US15/548,619 Active 2036-06-16 US10436096B2 (en) | 2015-02-05 | 2015-11-04 | Heat exchanger and method for controlling heat exchanger |
Country Status (6)
Country | Link |
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US (1) | US10436096B2 (en) |
EP (1) | EP3255340A4 (en) |
JP (1) | JP6632198B2 (en) |
KR (1) | KR101892887B1 (en) |
CN (1) | CN107208888B (en) |
WO (1) | WO2016125353A1 (en) |
Families Citing this family (6)
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WO2018139669A1 (en) * | 2017-01-30 | 2018-08-02 | 三菱日立パワーシステムズ株式会社 | Gas-to-gas heat exchanger |
CN109028569B (en) * | 2018-09-09 | 2024-01-05 | 无锡博众热能环保设备有限公司 | Flue gas full-cycle hot-blast stove |
CN109237505A (en) * | 2018-09-13 | 2019-01-18 | 华电电力科学研究院有限公司 | The device and its working method that water disappears white are received in a kind of classification waste heat recycling condensation of flue gas |
JP7311990B2 (en) * | 2019-03-22 | 2023-07-20 | 荏原環境プラント株式会社 | Exhaust heat recovery boiler and method for controlling temperature of heat transfer tube of exhaust heat recovery boiler |
CN111911947A (en) * | 2020-08-21 | 2020-11-10 | 邯郸学院 | Flue gas dehumidification system |
JP7203069B2 (en) * | 2020-09-08 | 2023-01-12 | 三菱重工パワー環境ソリューション株式会社 | Heat exchangers and flue gas treatment equipment |
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Also Published As
Publication number | Publication date |
---|---|
KR101892887B1 (en) | 2018-10-04 |
CN107208888A (en) | 2017-09-26 |
EP3255340A4 (en) | 2018-02-21 |
EP3255340A1 (en) | 2017-12-13 |
CN107208888B (en) | 2022-01-07 |
JP2016142515A (en) | 2016-08-08 |
JP6632198B2 (en) | 2020-01-22 |
KR20170102515A (en) | 2017-09-11 |
US20180010504A1 (en) | 2018-01-11 |
WO2016125353A1 (en) | 2016-08-11 |
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